MX166892B - Procedimiento para la obtencion de licor de maceracion de maiz - Google Patents

Procedimiento para la obtencion de licor de maceracion de maiz

Info

Publication number
MX166892B
MX166892B MX009737A MX973787A MX166892B MX 166892 B MX166892 B MX 166892B MX 009737 A MX009737 A MX 009737A MX 973787 A MX973787 A MX 973787A MX 166892 B MX166892 B MX 166892B
Authority
MX
Mexico
Prior art keywords
corn
water
procedure
obtaining corn
steep liquor
Prior art date
Application number
MX009737A
Other languages
English (en)
Inventor
Jean-Claude De Troostembergh
Francoise Oudenne
Original Assignee
Cpc International Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Cpc International Inc filed Critical Cpc International Inc
Publication of MX166892B publication Critical patent/MX166892B/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B30/00—Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
    • C08B30/04—Extraction or purification
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/14—Fungi; Culture media therefor
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B30/00—Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
    • C08B30/02—Preparatory treatment, e.g. crushing of raw materials or steeping process
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P37/00—Preparation of compounds having a 4-thia-1-azabicyclo [3.2.0] heptane ring system, e.g. penicillin
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S435/00—Chemistry: molecular biology and microbiology
    • Y10S435/813—Continuous fermentation

Abstract

La presente invención se refiere a un procedimiento para la obtención de licor de maceración de maíz, caracterizado por el hecho de que comprende a) separar el agua de maceración de maíz; b) ajustar inicialmente el pH del agua de maceración a por lo menos aproximadametne 3,5; c) mantener el agua de maceración de maíz a una temperatura de aproximadamente 40 grados hasta aproximadamente 48 grados C durante hasta 48 horas para el desarrollo de biomasa; d) alimentar continuamente agua de maceración de maíz a la biomasa desarrollada a un régimen tal que el tiempo de residencia está en un exceso de 4 horas en contacto con la biomasa a una temperatura de aproximadamente 40 hasta aproximadamente 48 grados C, ajustándose el pH de la alimentación de agua de maceración, por lo menos en la etapa inicial de operación continua, para que sea de por lo menos aproximadamente 3,5; y e) separar el agua de maceración de maíz de la biomasa y reducir su volumen por evaporación para dar un licor de maceración de maíz.
MX009737A 1986-12-15 1987-12-14 Procedimiento para la obtencion de licor de maceracion de maiz MX166892B (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB868629913A GB8629913D0 (en) 1986-12-15 1986-12-15 Corn steep liquor

Publications (1)

Publication Number Publication Date
MX166892B true MX166892B (es) 1993-02-11

Family

ID=10609022

Family Applications (1)

Application Number Title Priority Date Filing Date
MX009737A MX166892B (es) 1986-12-15 1987-12-14 Procedimiento para la obtencion de licor de maceracion de maiz

Country Status (21)

Country Link
US (1) US4980282A (es)
EP (1) EP0272049B1 (es)
JP (1) JP2590158B2 (es)
KR (1) KR960003619B1 (es)
CN (1) CN1009095B (es)
AT (1) ATE84800T1 (es)
AU (1) AU603626B2 (es)
BR (1) BR8706813A (es)
CA (1) CA1287313C (es)
DE (1) DE3783747T2 (es)
DK (1) DK655187A (es)
ES (1) ES2037097T3 (es)
FI (1) FI88169C (es)
GB (1) GB8629913D0 (es)
IE (1) IE59978B1 (es)
MX (1) MX166892B (es)
NO (1) NO169084C (es)
NZ (1) NZ222510A (es)
PT (1) PT86345B (es)
TR (1) TR25107A (es)
ZA (1) ZA878908B (es)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5922240A (en) * 1995-11-09 1999-07-13 Ice Ban Usa, Inc. Deicing composition and method
US5635101A (en) * 1996-01-22 1997-06-03 Janke George A Deicing composition and method
US6179926B1 (en) 1999-04-12 2001-01-30 Corn Products International, Inc. Process for steeping corn and steepwater having a low reducing sugar content made therefrom
US6946282B2 (en) * 2002-09-27 2005-09-20 Corn Products International, Inc. Process for decreasing the reducing sugars content of light steepwater
US20050123644A1 (en) * 2003-01-24 2005-06-09 Cargill, Incorporated Phosphate-containing fertilizer derived from steepwater
US20060169947A1 (en) * 2003-03-06 2006-08-03 Leist E G Deicing compositions and methods of use
US6861009B1 (en) * 2003-03-06 2005-03-01 E. Greg Leist Deicing compositions and methods of use
US20070110909A1 (en) * 2005-11-14 2007-05-17 Isakoff Louis A Reduction or elimination of microbial growth and biofouling of salted wet biomass byproducts
US7770358B2 (en) * 2007-01-17 2010-08-10 Parata Systems, Llc Devices for capping vials useful in system and method for dispensing prescriptions
GB0712175D0 (en) * 2007-06-23 2007-08-01 Salt Union Ltd De-icing method
WO2009018524A2 (en) 2007-08-02 2009-02-05 Douglas Joel S Magnus force fluid flow energy harvester
ES2435324B2 (es) 2012-06-18 2014-04-23 Universidade De Vigo Procedimiento de separación de los surfactantes presentes de licores de lavado de maíz y usos
CN102942632B (zh) * 2012-11-29 2014-08-27 黄龙食品工业有限公司 一种用于提高玉米浸泡效果的乳酸菌接种法
CN104719627B (zh) * 2015-04-13 2018-01-19 山东省鲁洲食品集团有限公司 一种可直接饲喂畜禽的玉米浆/干粉的处理方法

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2232555A (en) * 1939-10-07 1941-02-18 Musher Foundation Inc Processing corn
US2298623A (en) * 1940-04-08 1942-10-13 Clinton Company Steep water treatment
US2444176A (en) * 1945-05-05 1948-06-29 Staley Mfg Co A E Treatment of corn steepwater
ES421472A1 (es) * 1973-12-14 1976-06-16 Glucosa Proceso mejorado para maceracion de grano de cereales.
JPS561899A (en) * 1979-06-20 1981-01-10 Shige Motokazu Production of milo starch
FR2464298A1 (fr) * 1979-09-04 1981-03-06 Roquette Freres Procede de trempage du mais, produits ainsi obtenus et leur application a la fabrication de la penicilline
US4771001A (en) * 1986-03-27 1988-09-13 Neurex Corp. Production of lactic acid by continuous fermentation using an inexpensive raw material and a simplified method of lactic acid purification

Also Published As

Publication number Publication date
JPS63167787A (ja) 1988-07-11
AU8215187A (en) 1988-06-16
KR960003619B1 (ko) 1996-03-20
DK655187A (da) 1988-06-16
ZA878908B (en) 1988-05-25
EP0272049B1 (en) 1993-01-20
EP0272049A2 (en) 1988-06-22
ES2037097T3 (es) 1993-06-16
PT86345B (pt) 1990-11-07
NO169084C (no) 1992-05-06
FI88169C (fi) 1993-04-13
TR25107A (tr) 1992-09-28
NO875202D0 (no) 1987-12-14
EP0272049A3 (en) 1989-02-15
AU603626B2 (en) 1990-11-22
FI875482A (fi) 1988-06-16
NO875202L (no) 1988-06-16
DE3783747T2 (de) 1993-05-13
DK655187D0 (da) 1987-12-14
CN87101146A (zh) 1988-08-10
DE3783747D1 (de) 1993-03-04
NZ222510A (en) 1990-01-29
ATE84800T1 (de) 1993-02-15
CN1009095B (zh) 1990-08-08
KR880007014A (ko) 1988-08-26
JP2590158B2 (ja) 1997-03-12
BR8706813A (pt) 1988-07-19
IE873389L (en) 1988-06-15
PT86345A (en) 1988-01-01
CA1287313C (en) 1991-08-06
GB8629913D0 (en) 1987-01-28
IE59978B1 (en) 1994-05-04
NO169084B (no) 1992-01-27
US4980282A (en) 1990-12-25
FI875482A0 (fi) 1987-12-14
FI88169B (fi) 1992-12-31

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